FIELD: petroleum processing and petrochemistry.
SUBSTANCE: catalytic reforming of gasoline fractions is accomplished in a system constituted by several in series connected reactors at elevated pressure and hydrogen-containing gas circulation, wherein temperature of gas at first reactor inlet ranges from 380 to 470°C and in the other reactors 470-540°C. Reforming catalyst comprises alumina-supported platinum, fluorine, and optionally rhenium. In the first reactor, catalyst additionally contains 0.02 to 1.5% of fluorine.
EFFECT: increased yield and improved quality of product.
2 cl, 7 tbl, 7 ex
Title | Year | Author | Number |
---|---|---|---|
METHOD OF CATALYTIC REFORMING OF GASOLINE FRACTIONS | 1995 |
|
RU2081151C1 |
STRAIGHT-RUN GASOLINE FRACTION PROCESSING METHOD | 2005 |
|
RU2288941C1 |
PROCESS FOR CATALYTIC REFORMING OF GASOLINE FRACTIONS | 1992 |
|
RU2019557C1 |
METHOD OF CATALYTIC REFORMING OF GASOLINE FRACTIONS | 1996 |
|
RU2097404C1 |
METHOD OF CATALYTIC REFORMING OF GASOLINE FRACTIONS | 2007 |
|
RU2352612C1 |
PROCESS OF CATALYTIC REFORMING OF GASOLINE FRACTIONS ON ALUMINUM-PLATINUM-RHENIUM CATALYST | 2005 |
|
RU2281969C1 |
METHOD FOR CATALYTIC REFORMING OF GASOLINE FRACTIONS | 2020 |
|
RU2752382C1 |
METHOD FOR CATALYTIC REFORMING | 1996 |
|
RU2101322C1 |
METHOD OF PROCESSING LONG GASOLINE FRACTION | 2005 |
|
RU2289610C1 |
METHOD OF RECOVERY OF HIGH ANTIKNOCK GASOLINE AND AROMATIC HYDROCARBONS | 1992 |
|
RU2010838C1 |
Authors
Dates
2006-03-27—Published
2004-06-25—Filed